Abstract
For the purpose of the successful analysis of existing technologies, we will try to reproduce the main arguments that were likely made by the previous generations of process developers. On the one hand, it is interesting to retrace why the original ideas have established such a rigid paradigm that is widely shared by the industrial and scientific communities and, by force of habit, remains without any critical view till date. On the other hand, it becomes clear why the process layouts in many applications look so uniform even when it is not demanded by the physical or chemical nature [e.g., purification processes, including ultra-deep hydrodesulfurization (see Chap. 6)].
Access this chapter
Tax calculation will be finalised at checkout
Purchases are for personal use only
References
R.G. Maiti, K.D.P. Nigam, Gas-liquid distributors for trickle-bed reactors: A review. Ind. Eng. Chem. Res. 46(19), 6164–6182 (2007)
E.W. Thiele, Relation between catalytic activity and size of particle. J. Ind. Eng. Chem. 31, 916–920 (1939)
Y.B. Zeldowitch, To the theory of the reaction on a porous or powder catalyst. Acta Physicochimica USSR, 4, 583–592 (1939)
D. Murzin, T. Salmi, Catalytic Kinetics (Elsevier, Amsterdam, 2005)
R.E. Hayes, S.T. Kolaczkowski, Introduction to Catalytic Combustion (Gordon and Breach Science Publishers, Amsterdam, 1997)
A. Kadivar, M.T. Sadeghi, M.M. Gharebagh, Estimation of kinetic parameters for hydrogenation reaction using a genetic algorithm. Chem. Eng. Technol. 32(10), 1588–1594 (2009)
L.B. Datsevich, D.A. Muhkortov, Multiphase fixed-bed technologies. Comparative analysis of industrial processes (experience of development and industrial implementation). Appl. Catal. A 261(2), 143–161 (2004)
J.F. Jenck, Gas–liquid–solid reactors for hydrogenation in fine chemical synthesis, in Heterogeneous Catalysis and Fine Chemicals II, ed. by M. Guisnet, J. Barrault, C. Bouchoule, D. Duprez, G. Perot, R. Maurel, C. Montassier (Elsevier, Amsterdam, 1991), pp. 1–19
M. Herskowitz, Hydrogenation of benzaldehyde to benzyl alcohol in a slurry and fixed-bed reactor, in Heterogeneous Catalysis and Fine Chemicals II, ed. by M. Guisnet, J. Barrault, C. Bouchoule, D. Duprez, G. Perot, R. Maurel, C. Montassier (Elsevier, Amsterdam, 1991), pp. 105–112
C.N. Satterfield, Mass Transfer in Heterogeneous Catalysis (MIT Press, Cambridge, 1970)
H. Gierman, Design of laboratory hydrotreating reactors scaling down of trickle-flow reactors. Appl. Catal. 43, 277–286 (1988)
G. Mary, J. Chaouki, F. Luck, Trickle-bed laboratory reactors for kinetic studies. Int. J. Chem. Reactor Eng. 7, Review R2 (2009)
L. Harwell, S. Thakkar, S. Polcar, R.E. Palmer, Study outlines optimum ULSD hydrotreater design. Oil & Gas J. (2003)
L. Harwell, S. Thakkar, S. Polcar, R.E. Palmer, Study identifies optimum operating conditions for ULSD hydrotreaters. Oil & Gas J. (2003)
J.H. Gary, G.E. Handwerk, M.J. Kaiser, Petroleum Refining: Technology and Economics (CRC Press, Boca Raton, 2007)
P.R. Robinson, G.E. Dolbear, in Hydrotreating and hydrocracking: fundamentals, ed. by C.S. Hsu, P.R. Robinson. Practical Advances in Petroleum Processing, vol 1 (Springer, New York, 2006), 177–218
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
Copyright information
© 2012 The Author(s)
About this chapter
Cite this chapter
Datsevich, L.B. (2012). Traditional Approaches to the Design of Fixed-Bed Reactors. In: Conventional Three-Phase Fixed-Bed Technologies. SpringerBriefs in Applied Sciences and Technology, vol 7. Springer, New York, NY. https://doi.org/10.1007/978-1-4614-4836-5_3
Download citation
DOI: https://doi.org/10.1007/978-1-4614-4836-5_3
Published:
Publisher Name: Springer, New York, NY
Print ISBN: 978-1-4614-4835-8
Online ISBN: 978-1-4614-4836-5
eBook Packages: Chemistry and Materials ScienceChemistry and Material Science (R0)